BACKGROUND OF THE INVENTION
[0001] The present invention relates to a nickel plating solution to which a salt of an
element in Group IIa in the periodic table is added, a method of copper-nickel-chromium
or nickel-chromium bright electroplating and a film obtained by such a plating method.
The nickel plating film is a bright electroplating film having excellent corrosion
resistance.
[0002] Copper-nickel-chromium plating or nickel-chromium plating with excellent corrosion
resistance is frequently made on the surfaces of automobile cars, electrical products
and parts thereof for the purpose of improving the corrosion resistance of the basic
materials and improving the decorative effect by combination with decorating.
[0003] However, since flaws or cracks easily occur in the chromium surface platings obtained
by such copper-nickel-chromium plating or nickel-chromium plating, corrosion is significantly
progressed to the insides of the platings from the defective portions in the surfaces
due to the presence of the flaws or cracks. This corrosion rapidly proceeds and finally
reaches the basic materials because of the small anode area (nickel) and high corrosion
current density. There is thus a great possibility that the corrosion of the basic
materials brings about the occurrence of not only defects in the appearances but also
fatal defects.
[0004] In order to cope with this problem, therefore, the thickness of each metal deposit
is increased, or a plurality of deposits of each metal are laminated. However, such
a method has a problem from the viewpoints of effective utilization of resources and
cost.
[0005] The specification of Japanese Patent Publication No. 56-15471 discloses a corrosion-resistant
metal film which is obtained by nickel plating using a semi-bright nickel plating
and bright nickel plating solutions to each of which a brightener and a wetting agent
are added, and a nickel plating solution to which a soluble amine compound and a metal
selected from Groups III, V and VI in the periodic table, preferably aluminum or chromium,
is added, so that fine particles are deposited on the nickel plating; and then chromium
plating the nickel plating so that the local corrosion current density is decreased
by the formation of micropores in the surface of the chromium plating, thereby improving
the corrosion resistance.
[0006] The aforementioned prior art also has problems in that plating must be effected within
a narrow control range for preventing the occurrence of dulling on the film formed
after chromium plating and in that yellowing detrimental to plating occurs if the
amount of the metal ions added exceeds 0.5 g/l, and such detrimental substance must
be removed.
SUMMARY OF THE INVENTION
[0007] It is an object of the present invention to provide a nickel plating solution which
permits the solution of all the above-described problems of prior art, a method of
copper-nickel-chromium electroplating or nickel-chromium electroplating using the
plating solution and a plating film obtained by the nickel-chromium or copper-nickel-chromium
electroplating method.
[0008] It is a first object of the present invention to provide a nickel plating solution
which contains nickel or a nickel salt and 0.5 to 20 g/l of salt of an element in
Group IIa in the periodic table.
[0009] It is a second object of the present invention to provide a copper-nickel-chromium
bright electroplating method or a nickel-chromium bright electroplating method comprising
the steps of nickel eutectoid plating with a thickness of 0.2 to 50 µm using as a
nickel plating bath a nickel plating solution containing nickel or a nickel salt and
0.5 to 20 g/l of salt of an element of Group IIa in the periodic table during copper-nickel-chromium
electroplating or nickel-chromium electroplating on a basic material; and then chromium
plating with a thickness of 0.1 to 1.0 µm to form a plating having excellent corrosion
resistance.
[0010] It is a third object of the present invention to provide a copper-nickel-chromium
or nickel-chromium bright electroplating film with excellent corrosion resistance
which is formed by the copper-nickel-chromium electroplating method or the nickel-chromium
electroplating method provided by the second object, which has a thickness of 0.2
to 50 µm, micropores and the copper and nickel layers formed on the basis material
or the nickel layer formed directly on the basis material by eutectoid plating.
BRIEF DESCRIPTION OF THE DRAWINGS
[0011]
Fig. 1 is an explanatory view which shows the corrosion mechanism in a plating film
in accordance with the present invention; and
Fig. 2 is a drawing which shows the corrosion mechanism in a conventional plating
film.
DETAILED DESCRIPTION OF THE INVENTION
[0012] As a result of research performed by the inventor with a view to solving the above-described
problems of prior art, the inventor discovered a copper-nickel-chromium or nickel-chromium
electroplating method of forming bright electroplating film with excellent corrosion
resistance, comprising the steps of eutectoid plating with a thickness of 0.2 to 50
µm by using as a nickel plating bath a nickel plating solution containing nickel or
a nickel salt and 0.2 to 50 g/l of salt of an element in Group IIa in the periodic
table; and then chromium plating with a thickness of 0.1 to 1.0 µm.
[0013] The nickel plating solution contained in the present invention is obtained by adding
0.5 to 20 g/l of one, two or three salts of elements in Group IIa in the periodic
table to a Watts bath, a Weisberg bath, a sulfamate bath or a chloride bath.
[0014] The nickel or nickel salt used in the nickel plating solution of the present invention
is nickel or a nickel salt of the type that is generally used in nickel plating. Examples
of nickel salts include nickel chloride, nickel sulfate, nickel sulfamate and the
like.
[0015] Examples of salts of elements in Group IIa in the periodic table include beryllium
salts such as beryllium oxide, beryllium sulfate and the like; magnesium salts such
as magnesium chloride, magnesium oxide, magnesium hydroxide, magnesium phosphate,
magnesium carbonate, magnesium nitrate, magnesium sulfate, magnesium acetate, magnesium
bromide, magnesium fluoride, magnesium silicate and the like; calcium salts such as
calcium chloride, calcium hydroxide, calcium carbonate, calcium nitrate, calcium acetate,
calcium phosphate, calcium bromide, calcium carbide, calcium fluoride, calcium iodide,
calcium oxalate, calcium silicate and the like; strontium salts such as strontium
hydroxide, strontium oxalate, strontium chromate, strontium oxide, strontium carbonate,
strontium sulfate, strontium nitrate, strontium chloride, strontium acetate, strontium
fluoride and the like; barium salts such as barium chloride, barium sulfate, barium
nitrate, barium carbonate, barium sulfate, barium hydroxide, barium oxide, barium
fluoride, barium acetate, barium formate, barium iodide, barium phosphate and the
like.
[0016] Strontium salts and calcium salts are preferable, and strontium chloride and calcium
carbonate are more preferable.
[0017] If the adding amount of the element in Group IIa in the periodic table is 0.5 g/l
or less, no effectiveness is recognized. If the amount is 20 g/l or more, the salt
of the same element settles out and adheres to the heating tube and the electrode
plates in the plating tank used. This causes the deteriorate in thermal efficiency,
electrodeposition efficiency and appearance of the film formed. A eutectoid of a salt
of any one of the above elements is formed on the film obtained by nickel plating
using the plating solution of the present invention, and micropores are formed in
the film obtained after chromium plating on the nickel film.
[0018] Examples of plating basis materials that may be used in the present invention include
basis materials of metals such as iron, copper, zinc, aluminum and the like; and various
resins such as ABS resins (acrylonitrile-butadiene-styrene resins), PPO resins (polyphenyleneoxide
resins), polyacetal resins, polyamide resins, polycarbonate resins, PP resins (polypropylene
resins), PPS resins (polyphenylene sulfide resins), epoxy resins and the like, all
of which resins are made conductive by predetermined treatment.
[0019] Pretreatment of a metal basic material such as an iron material or the like is performed
by a usual pretreatment method, for example, comprising the following steps:
(1) Abrasion of basic material
(2) Hanging ( a material to be plated is hung on a plating jig)
(3) Washing (washing by immersion in an alkali, acid or alkali electrolysis, a solvent
or degreasing)
(4) Acid immersion (treatment using an acid selected from the group consisting of
hydrochloric acid, sulfuric acid, fluoric acid, nitric acid and the like in correspondence
with the basic material used)
(5) Metal substitution (depending upon the kind of the metal used, for example, in
a case of aluminum, the surface of aluminum is substituted by a zinc salt)
[0020] If required, a washing step is interposed between the respective steps.
[0021] When a resin basic material is used, pretreatment is effected by a usual pretreatment,
for example, comprising the following steps:
(1) Molding
(2) Hanging
(3) Washing (washing by immersion in an alkali or acid or degreasing treatment)
(4) Pre-etching (for example, PP resin is sometimes treated with xylol or the like
for 15 to 20 minutes under heating)
(5) Etching (treatment with chromic anhydride and sulfuric acid under heating)
(6) Catalyzation (treatment with stannous chloride and hydrochloric acid at room temperature)
(7) Activation (palladium chloride and hydrochloric acid at room temperature)
(8) Chemical plating (plating with chemical copper and chemical nickel)
[0022] If required, a washing step is interposed between the respective steps.
[0023] In the present invention, copper-nickel-chromium electroplating on the basic material
is basically carried out by a general method. However, the method of the present invention
is characterized by using as a nickel plating solution the above-described nickel
plating solution of the present invention.
[0024] The method of copper-nickel-chromium electroplating the basic material which is previously
treated by the above-mentioned pretreatment method, for example, comprises the following
steps:
(1) Acid or alkali immersion
(2) Copper strike electroplating
(3) Copper electroplating
(4) Nickel electroplating
(5) Chromium electroplating
[0025] In Step (1) of acid or alkali immersion, the basic material which is previously subjected
to the above-described pretreatment is activated by immersing it in a 1 to 5 wt%
solution of a mineral acid such as sulfuric acid, hydrochloric acid or the like or
a 1 to 5 wt% solution of an alkali such as sodium hydroxide or the like. The treatment
time is about 1 to 5 minutes.
[0026] The basic material which is subjected to the treatment is preferably washed with
water and then supplied to the next Step (2).
[0027] In Step (2) of copper strike electroplating, a thin copper plating film having good
adhesion is formed on the basis material by a general strike plating method using
copper pyrophosphate under the condition of a cathode current density of 1 to 5 A/Cm².
[0028] In Step (3), copper electroplating is effected by using a general acid bath containing
copper sulfate and sulfuric acid. An alkali bath or a bath obtained by dissolving
copper cyanide in an alkali cyanide may be used.
[0029] In this case, a brightener such as thiourea, sodium 5-naphthalenedisulfonate, 2-butyne-1,4-diol,
gelatin, glue, dextrin or the like; or a semi-brightener may be added to the plating
bath by a normal method so that brightness or semi-brightness can be obtained.
[0030] Step (4) of nickel electroplating is a characteristic step of the present invention
in which electroplating is first effected by a general nickel electroplating method
using a nickel plating bath such as a Watts bath (nickel sulfate, nickel chloride,
boric acid), a Weisberg bath (nickel sulfate, cobalt sulfate, boric acid, nickel chloride),
a sulfamate acid bath (nickel sulfamate, boric acid), a chloride bath (nickel chloride,
boric acid) or the like. Nickel electroplating is then performed by using a nickel
plating bath of the present invention obtained by adding a 0.5 to 20 g/l of salt of
an element in Group IIa in the periodic table to the above nickel plating bath. Alternatively,
nickel electroplating on the basic material plated with copper in Step (3) is directly
performed by using the nickel plating bath of the present invention, without general
nickel electroplating being previously made. In this case, the thickness of the nickel
deposit formed is 2 to 50 µm, preferably 1.0 µm.
[0031] A brightener may be added to the nickel plating bath.
[0032] In Step (5), chromium electroplating is performed by a general plating method, for
example, using a chromium bath obtained by adding at least one of sulfuric acid, hydrogen
fluoride, ammonium fluoride and silicofluorides to anhydrous chromium oxide to form
a chromium deposit with a thickness of 0.1 to 1.0 µm on the nickel deposit.
[0033] A water washing step may be interposed between the respective steps.
[0034] In the present invention, although nickel-chromium electroplating on the basic material
is basically performed by a normal method, the method of the present invention is
characterized by using as a nickel plating bath the above-described nickel plating
bath of the present invention.
[0035] The nickel-chromium plating on the basic material which is previously subjected to
the pretreatment is effected by a general nickel-chromium electroplating method, for
example, comprising the following steps:
(1) Acid or alkali immersion
(2) Nickel electroplating
(3) Chromium electroplating
[0036] Steps (1), (2) and (3) in the method are respectively performed by the same methods
as those of the above-described Steps (1), (4) and (5).
[0037] The film obtained by the method of the present invention comprises a nickel deposit
which is formed on the basis material so that fine particles of a eutectoid of the
salt of the element in Group IIa in the periodic table, which is contained in the
nickel plating bath, are dispersed therein; and a chromium deposit which is formed
on the upper surface of the nickel deposit and has a thickness of 0.1 to 1.0 µm, the
surface chromium deposit having micropores in the surface thereof.
[0038] In the deposit formed by a conventional plating method shown in Fig. 2, local cells
are formed in portions where flaws or cracks occur and thus produce electrolytic reaction
therein. This reaction causes not only the significant dissolution of nickel due to
a small cathode (nickel) area but also the dissolution of the basic material metal.
There is thus a danger of creating fatal defects.
[0039] In the plating method in accordance with the present invention, the salt of the element
in Group IIa in the periodic table, which is contained in the nickel plating bath,
is dispersed or dissolved in the plating bath, and the eutectoid is produced in both
forms of an element and a salt. As shown in Fig. 1, the local cells are dispersed
by the micropores which are formed by the eutectoid of the metal added or the salt
thereof so that the electromotive force and the dissolution of nickel can be reduced.
In addition, the formation of the eutectoid of the element added causes the passivation
of nickel and thus causes the control and prevention of dissolution of nickel and
an improvement in corrosion resistance.
EXAMPLE
[0040] Examples of the present invention are described below. Example 1
[0041] Copper-nickel-chromium electroplating was performed on a basic material of ABS resin,
which had been subjected to predetermined pretreatment in accordance with the steps
below.
(1) Acid immersion |
Solution composition |
|
Sulfuric acid |
25 - 80 g/l |
Bath temperature |
room temperature |
Immersion |
5 seconds - 1 minute |
Water washing |
|
(2) Copper strike plating |
Solution composition |
|
Copper pyrophosphate trihydrate |
15 - 25 g/l |
Potasium pyrophosphate |
60 - 100 g/l |
Potassium oxalate |
10 15 g/l |
P ratio |
11 - 13 |
Bath temperature |
40 - 50°C |
pH |
8 - 9 |
Average cathode current density |
1 - 5 A/Cm² |
Agitation |
air agitation |
Water washing |
|
(3) Acid immersion |
Solution composition |
|
Sulfuric acid |
30 - 60 g/l |
Bath temperature |
room temperture |
Immersion |
5 seconds - 1 minute |
(4) Copper plating |
Solution composition |
|
Copper sulfate pentahydrate |
150 - 200 g/l |
Sulfuric acid |
50 - 90 g/l |
Hydrochloric acid |
40 - 100 g/l |
Primary brightener (thiourea) |
3 - 7 ml/l |
Secondary brightener (dextrin) |
0.5 = 1 ml/l |
Bath temperature |
15 - 25°C |
Average cathode current density |
1 - 5 A/dm² |
Agitation |
air agitation |
(5) Acid immersion |
Solution composition |
|
Hydrochloric acid |
5 - 10 g/l |
Bath temperature |
room temperature |
Immersion |
30 seconds - 1 minute |
(6) Semi-bright nickel plating |
Solution composition |
|
Nickel sulfate hexahydrate |
250 - 350 g/l |
Nickel chloride hexahydrate |
35 - 50 g/l |
Boric acid |
30 - 60 g/l |
Brightener (sodium 5-naphthalenedisulfonate) |
0.1 - 0.2 g/l |
Bath temperature |
40 - 60°C |
pH |
3.5 - 4.5 |
Average cathode current density |
1 - 5 A/dm² |
Agitation |
air agitation |
Water washing |
|
(7) Bright nickel plating |
Solution composition |
|
Nickel sulfate hexahydrate |
250 - 360 g/l |
Nickel chloride hexahydrate |
35 - 60 g/l |
Boric acid |
30 - 50 g/l |
Primary brightener (sodium 1,5-naphthalenedisulfonate |
5 - 40 g/l |
Secondary brightener (2-butyne-1,4-diol) |
0.1 - 10 g/l |
Bath temperature |
40 - 60°C |
pH |
3.5 - 4.5 |
Average cathode current density |
1 - 5 A/dm² |
Agitation |
air agitation |
Water washing |
|
(8) Nickel plating using the nickel solution of the present invention |
Solution composition |
|
Nickel sulfate hexahydrate |
300 g/l |
Nickel chloride hexahydrate |
60 g/l |
Boric acid |
40 g/l |
Calcium carbonate |
2 g/l |
Strontium chloride |
1 g/l |
Bath temperature |
50 - 60°C |
pH |
3.8 - 4.5 |
Average cathode current density |
1 - 5 A/dm² |
Agitation |
air agitation |
Thickness |
2 µm |
(9) Chromium plating |
Solution composition |
|
Chromic anhydride |
15 - 400 g/l |
Sulfuric acid |
0.5 - 4 g/l |
Silicofluoride |
0.5 - 10 g/l |
Bath temperature |
35 - 55°C |
Average cathode current density |
5 - 25A/Cm² |
Water washing |
|
[0042] The plating film obtained had good bright appearance.
Example 2
[0043] Plating was carried out by the same method as in Example 1 with the exception that
the solution composition and the conditions of step (8) of Example 1 were changed
as described below.
Solution composition |
|
Nickel sulfate hexahydrate |
220 g/l |
Nickel chloride hexahydrate |
40 g/l |
Boric acid |
40 g/l |
Calcium carbonate |
5 g/l |
Strontium chloride |
3 g/l |
Bath temperature |
50 - 60°C |
pH |
4.5 - 5.0 |
Average cathode current density |
0.5 - 4 A/dm² |
Agitation |
air agitation |
Thickness |
0.2 µm |
[0044] The plating film obtained had micropores and good bright appearance.
Example 3
[0045] Nickel-chromium electroplating was performed on the basic material, which had been
subjected to the predetermined pretreatment, in accordance with the following steps:
(1) Acid immersion |
Solution composition |
|
Sulfuric acid |
25 - 80 g/l |
Bath temperature |
room temperature |
Immersion |
5 seconds to 1 minute |
Water washing |
|
(2) Semi-bright nickel plating |
Solution composition |
|
Nickel sulfate hexahydrate |
250 - 350 g/l |
Nickel chloride hexahydrate |
35 - 50 g/l |
Boric acid |
30 - 60 g/l |
Brightener (sodium 5-naphthalenedisulfonate |
0.1 - 0.2 g/l |
Bath temperature |
40 - 60°C |
pH |
3.5 - 4.5 |
Average cathode current density |
1 - 5 A/dm² |
Agitation |
air agitation |
Water washing |
|
(3) Bright nickel plating |
Solution composition |
|
Nickel sulfate hexahydrate |
250 - 360 g/l |
Nickel chloride hexahydrate |
35 - 60 g/l |
Boric acid |
30 - 50 g/l |
Primary brightener (sodium 1,5-naphthalenedisulfonate) |
5 - 40 g/l |
Secondary brightener (2-butyne-1,4-diol) |
0.1 - 10 g/l |
Bath temperature |
40 - 60°C |
pH |
3.5 - 4.5 |
Average cathode current density |
1 - 5 A/dm² |
Agitation |
air agitation |
Water washing |
|
(4) Nickel plating using the nickel solution of the present invention |
Solution composition |
|
Nickel sulfate hexahydrate |
300 g/l |
Nickel chloride hexahydrate |
60 g/l |
Boric acid |
40 g/l |
Calcium carbonate |
2 g/l |
Strontium chloride |
1 g/l |
Bath temperature |
50 - 60°C |
pH |
3.8 - 4.5 |
Average cathode current density |
1 - 5 A/dm² |
Agitation |
air agitation |
Thickness |
2 µm |
Water washing |
|
(5) Chromium plating |
Solution composition |
|
Chromic anhydride |
150 - 400 g/l |
Sulfuric acid |
0.5 - 4 g/l |
Silicofluoride |
0.5 - 10 g/l |
Bath temperature |
35 - 55°C |
Average cathode current density |
5 - 25 A/Cm² |
Water washing |
|
Example 4
[0046] Nickel plating was effected by the same method as in Example 1 with the exception
that step (6) of Example 1 were removed and the solution compositions and the conditions
of Steps (7) and (8) of Example 1 were changed as described below.
(7)′ Bright nickel plating (Weisberg bath) |
Solution composition |
|
Nickel sulfate hexahydrate |
240 - 300 g/l |
Nickel chloride hexahydrate |
30 - 45 g/l |
Boric acid |
30 - 40 g/l |
Cobalt sulfate |
12 - 15 g/l |
Formic acid |
25 - 30 g/l |
Formalin |
1.5 - 2.5 g/l |
Bath temperature |
55 - 60°C |
PH |
3.7 - 4.2 |
Average cathode current density |
3 - 8 A/dm² |
Agitation |
air agitation |
Water washing |
|
(8)′ Nickel plating in accordance with the present invention |
Solution composition |
|
Nickel sulfate hexahydrate |
300 g/l |
Nickel chloride hexahydrate |
60 g/l |
Boric acid |
40 g/l |
Calcium carbonate |
2 g/l |
Strontium chloride |
1 g/l |
Bath temperature |
50 - 60°C |
PH |
3.8 - 4.5 |
Average cathode current density |
1 - 5 A/dm² |
Agitation |
air agitation |
Thickness |
1 µm |
[0047] The plating film obtained had a reproducible substrate and good appearance with brightness.
[0048] The method of the present invention was compared with a conventional method in order
to show that the film obtained by the method of the present invention has excellent
properties.
[0049] The sample plated in Example 1 of the present invention was compared with the sample
plated in Example 3-(d) (Comparative Example) of the specification of Japanese Patent
Publication No. 56-15471, which was selected as a conventional method, by CASS tests
in accordance with JISDO201 Appendix 2.
Comparative Example
[0050]

[0051] Nickel plating was effected by using a solution having a pH value of 3, which was
obtained by adding to the above plating solution 0.2 g/l of sodium diethylenetriamine-pentaacetate,
12.5 mg/l of aluminum sulfate and 5 mg/l of chromium sulfate, at 60.0 too 62.8°C under
air agitation. Chromium plating was then effected.
Table 1
Kind of Basis |
Plating Condition (thickness, mm) |
CASS test after 32 h |
Material |
Cu |
SNi |
BNi |
Intermediate |
Cr |
|
Iron |
- |
10 |
5 |
Example 1 |
0.1 |
9.0 |
Iron |
- |
10 |
5 |
Comparative Example |
0.1 |
6.5 |
ABS resin |
10 |
10 |
5 |
Example 1 |
0.1 |
9.5 |
ABS resin |
10 |
10 |
5 |
Comparative Example |
0.1 |
7.0 |
* Cu : Copper |
SNi: Semi-bright nickel plating |
BNi: Bright nickel plating |
Cr: Chromium plating |
* Evaluation numerals shown in the table represent rating numbers. |
[0052] As described above, the present invention permits the formation of an electroplating
film which has micropores and corrosion resistance more excellent than that obtained
by a conventional plating method. A sufficient corrosive effect can be obtained even
if the thickness of a film is reduced, as compared with conventional films. In addition,
since the components of the plating solution can be easily analyzed, the plating bath
can be simply controlled. The present invention is therefore useful in the industrial
field.